AU6373399A - Method for polymerising epsilon-caprolactam to polyamide-6 - Google Patents
Method for polymerising epsilon-caprolactam to polyamide-6Info
- Publication number
- AU6373399A AU6373399A AU63733/99A AU6373399A AU6373399A AU 6373399 A AU6373399 A AU 6373399A AU 63733/99 A AU63733/99 A AU 63733/99A AU 6373399 A AU6373399 A AU 6373399A AU 6373399 A AU6373399 A AU 6373399A
- Authority
- AU
- Australia
- Prior art keywords
- effected
- caprolactam
- molten phase
- reactor
- polyamide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0053—Details of the reactor
- B01J19/0066—Stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
- B01J10/002—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor carried out in foam, aerosol or bubbles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1887—Stationary reactors having moving elements inside forming a thin film
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
- C08G69/08—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from amino-carboxylic acids
- C08G69/14—Lactams
- C08G69/16—Preparatory processes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G69/00—Macromolecular compounds obtained by reactions forming a carboxylic amide link in the main chain of the macromolecule
- C08G69/02—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids
- C08G69/08—Polyamides derived from amino-carboxylic acids or from polyamines and polycarboxylic acids derived from amino-carboxylic acids
- C08G69/14—Lactams
- C08G69/16—Preparatory processes
- C08G69/18—Anionic polymerisation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00761—Details of the reactor
- B01J2219/00763—Baffles
- B01J2219/00779—Baffles attached to the stirring means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/18—Details relating to the spatial orientation of the reactor
- B01J2219/182—Details relating to the spatial orientation of the reactor horizontal
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
- B01J2219/332—Details relating to the flow of the phases
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Dispersion Chemistry (AREA)
- Polyamides (AREA)
Abstract
The invention relates to a method for the hydrolytic polymerisation of epsi-caprolactam to polyamide-6, comprising a step (a) in which ring opening of part of the epsi-caprolactam to the corresponding amino caproic acid is effected in the presence of water and a step (b) in which polyaddition and polycondensation are effected under preferably anhydrous reaction conditions, in which at least one of the steps (a) and (b) is carried out in a reactor in which a self-renewing interface between the molten phase and the gas phase with a large surface/volume ratio of the molten phase is effected. The method is preferably effected in an horizontal scraped-surface reactor, since relatively strong mixing of the molten phase can be achieved in these and the molten phase is present in a thin layer, a large gas volume is present having a relatively high partial pressure of the water vapour and the thin layer is constantly renewed by shear forces. The method can be carried out in one reactor, preferably with several reaction zones, or with several reactors in series.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL1010373A NL1010373C2 (en) | 1998-10-22 | 1998-10-22 | Process for the polymerization of èpsilon-caprolactam to polyamide-6. |
NL1010373 | 1998-10-22 | ||
PCT/NL1999/000657 WO2000023502A1 (en) | 1998-10-22 | 1999-10-22 | METHOD FOR POLYMERISING ε-CAPROLACTAM TO POLYAMIDE-6 |
Publications (1)
Publication Number | Publication Date |
---|---|
AU6373399A true AU6373399A (en) | 2000-05-08 |
Family
ID=19768005
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU63733/99A Abandoned AU6373399A (en) | 1998-10-22 | 1999-10-22 | Method for polymerising epsilon-caprolactam to polyamide-6 |
AU63732/99A Abandoned AU6373299A (en) | 1998-10-22 | 1999-10-22 | Method for polymerising epsilon-caprolactam to polyamide-6 |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU63732/99A Abandoned AU6373299A (en) | 1998-10-22 | 1999-10-22 | Method for polymerising epsilon-caprolactam to polyamide-6 |
Country Status (12)
Country | Link |
---|---|
US (1) | US6566487B2 (en) |
EP (1) | EP1141089B1 (en) |
JP (1) | JP4237412B2 (en) |
KR (1) | KR100600932B1 (en) |
CN (1) | CN1158332C (en) |
AT (1) | ATE224417T1 (en) |
AU (2) | AU6373399A (en) |
DE (1) | DE69903069T2 (en) |
ID (1) | ID28449A (en) |
NL (1) | NL1010373C2 (en) |
TW (1) | TWI225496B (en) |
WO (2) | WO2000023502A1 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1148077A1 (en) * | 2000-04-21 | 2001-10-24 | Dsm N.V. | Process for the simultaneous preparation of polymers of caprolactam with at least two different viscosities |
KR100759658B1 (en) * | 2000-04-21 | 2007-09-17 | 코닌클리즈케 디에스엠 엔.브이. | Process for the simultaneous preparation of polyamides with at least two different viscosities |
DE10155242A1 (en) * | 2001-11-09 | 2003-05-22 | Bayer Ag | Manufacture of polyamide |
US7775276B2 (en) | 2006-03-03 | 2010-08-17 | Halliburton Energy Services, Inc. | Method and apparatus for downhole sampling |
HUE033035T2 (en) | 2010-04-14 | 2017-11-28 | Wingspeed Ag | Method for producing modified polyamide 6 |
CN104480561B (en) * | 2014-12-12 | 2016-08-24 | 东华大学 | A kind of caprolactam hydrolytic polymerization fibres and spinning process thereof |
CN111100287B (en) * | 2018-10-26 | 2023-01-20 | 中国石油化工股份有限公司 | Method for producing high-viscosity polyamide |
CN113522194A (en) * | 2021-06-30 | 2021-10-22 | 海阳科技股份有限公司 | Pigment low-temperature homogenization polyamide-6 in-situ polymerization reaction device and process thereof |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL73803C (en) * | 1947-11-28 | |||
US3565866A (en) * | 1964-09-17 | 1971-02-23 | Basf Ag | Continuous polymerization of lactams |
DE2558480C2 (en) * | 1975-12-24 | 1985-03-07 | Basf Ag, 6700 Ludwigshafen | Process for the polymerization of epsilon-caprolactam |
US4204049A (en) * | 1976-11-19 | 1980-05-20 | Basf Aktiengesellschaft | Hydrolytic polymerization of epsilon-caprolactam |
DE2821686A1 (en) * | 1978-05-18 | 1979-11-22 | Bayer Ag | PROCESS FOR PRODUCING LOW MONOMER AND LOW DIMER POLYAMIDES |
DE2918828A1 (en) * | 1979-05-10 | 1980-11-20 | Basf Ag | METHOD FOR THE CONTINUOUS PRODUCTION OF POLYCAPROLACTAM AND A DEVICE FOR CARRYING OUT THE METHOD |
JP2530780B2 (en) * | 1991-08-22 | 1996-09-04 | 宇部興産株式会社 | Method and apparatus for continuous polymerization of laurolactam |
DE19525319B4 (en) | 1995-07-12 | 2006-12-28 | Degussa Ag | Process for the discontinuous production of polylaurolactam |
-
1998
- 1998-10-22 NL NL1010373A patent/NL1010373C2/en not_active IP Right Cessation
-
1999
- 1999-10-13 TW TW088117711A patent/TWI225496B/en not_active IP Right Cessation
- 1999-10-22 DE DE69903069T patent/DE69903069T2/en not_active Expired - Lifetime
- 1999-10-22 ID IDW20010890A patent/ID28449A/en unknown
- 1999-10-22 AU AU63733/99A patent/AU6373399A/en not_active Abandoned
- 1999-10-22 AT AT99951264T patent/ATE224417T1/en not_active IP Right Cessation
- 1999-10-22 EP EP99951264A patent/EP1141089B1/en not_active Expired - Lifetime
- 1999-10-22 CN CNB998147117A patent/CN1158332C/en not_active Expired - Fee Related
- 1999-10-22 WO PCT/NL1999/000657 patent/WO2000023502A1/en active IP Right Grant
- 1999-10-22 KR KR1020017004891A patent/KR100600932B1/en not_active IP Right Cessation
- 1999-10-22 JP JP2000577222A patent/JP4237412B2/en not_active Expired - Fee Related
- 1999-10-22 WO PCT/NL1999/000656 patent/WO2000023501A1/en active Application Filing
- 1999-10-22 AU AU63732/99A patent/AU6373299A/en not_active Abandoned
-
2001
- 2001-06-22 US US09/886,374 patent/US6566487B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
TWI225496B (en) | 2004-12-21 |
ATE224417T1 (en) | 2002-10-15 |
CN1331717A (en) | 2002-01-16 |
WO2000023502A1 (en) | 2000-04-27 |
WO2000023501A1 (en) | 2000-04-27 |
NL1010373C2 (en) | 2000-04-26 |
KR20010080238A (en) | 2001-08-22 |
DE69903069D1 (en) | 2002-10-24 |
AU6373299A (en) | 2000-05-08 |
JP2002527591A (en) | 2002-08-27 |
ID28449A (en) | 2001-05-24 |
KR100600932B1 (en) | 2006-07-13 |
EP1141089B1 (en) | 2002-09-18 |
US6566487B2 (en) | 2003-05-20 |
US20020002266A1 (en) | 2002-01-03 |
CN1158332C (en) | 2004-07-21 |
JP4237412B2 (en) | 2009-03-11 |
EP1141089A1 (en) | 2001-10-10 |
DE69903069T2 (en) | 2003-05-22 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MK6 | Application lapsed section 142(2)(f)/reg. 8.3(3) - pct applic. not entering national phase |